US10113062B2ActiveUtilityA1
Modified polylactic acid, polymeric blends and methods of making the same
Est. expiryFeb 18, 2031(~4.6 yrs left)· nominal 20-yr term from priority
C08L 23/12C08L 67/04C04B 40/0245C04B 38/0054C04B 28/18F17C 11/002C04B 38/0074B29C 49/0005Y10T428/31797Y10T428/31515C08L 15/00B32B 2250/24B32B 27/36B32B 7/12Y10T428/139B32B 2270/00B32B 27/32C08G 63/912B29C 45/0001B29C 51/002C08L 23/10B32B 27/08B29K 2067/046B29C 48/09B29C 48/05B29C 48/21B29C 48/08B29C 48/022
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Claims
Abstract
Polymeric compositions and processes of forming the same are discussed herein. The processes generally include contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A process for forming a polymeric composition comprising:
contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof; and
contacting the polylactic acid and the reactive modifier with a polyolefin to produce a polyolefin-polylactic acid blend, wherein the polyolefin exhibits a melt flow rate of less than about 6 dg/min.
2. The process of claim 1 , wherein the polyolefin exhibits a melt flow rate ranging from about 0.5 dg/min. to about 6 dg/min.
3. The process of claim 1 , wherein the polylactic acid is selected from poly(D-lactide), poly(L-lactide), poly(DL-lactide), and combinations thereof.
4. The process of claim 1 , wherein the polylactic acid has a concentration of from about 2 wt. % to about 98 wt. % based on the total weight of the polymeric composition.
5. The process of claim 1 , wherein the reactive modifier contacts the polylactic acid in a concentration of from about 2 wt. % to about 30 wt. % based on the total weight of the polymeric composition.
6. The process of claim 1 , wherein the reactive modifier is an epoxy-functionalized polybutadiene oligomer.
7. The process of claim 6 , wherein the epoxy-functionalized polybutadiene oligomer has a number average molecular weight in a range from about 500 g/mol to about 20000 g/mol.
8. The process of claim 1 , wherein the reactive modifier is an ionic monomer.
9. The process of claim 8 , wherein the ionic monomer is an organometallic salt having acrylate functional groups.
10. The process of claim 1 , wherein the polyolefin is selected from polypropylene, polyethylene, copolymers thereof and combinations thereof.
11. The process of claim 1 , wherein the polyolefin has a concentration of from about 2 wt. % to about 98 wt. % based on the total weight of the polymeric composition.
12. The process of claim 1 , further comprising processing the polymeric composition using fiber extrusion or coextrusion.
13. A process comprising:
forming a polymeric composition by contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof;
processing the polymeric composition using one or more polymer processing techniques selected from: film, sheet, pipe extrusion or coextrusion, blow molding, injection molding, rotary molding, and thermoforming.Cited by (0)
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